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Curriculum research on Sustainable Development
Education in Chinese Higher Education – Education for
SD, SD for Education
Tongzhen Zhu
To cite this version:
Laser-induced Nucleation in a
Coaxial Microfluidic Mixer
Thèse de doctorat de l'Université Paris-Saclay
École Normale Supérieure Paris-Saclay
École doctorale n°573 Interfaces : approches interdisciplinaires,
fondements, applications et innovation (Interfaces)
Spécialité de doctorat : ChimieThèse présentée et soutenue à Cachan, le 13 Juin 2019, par
Zhengyu Zhang
Composition du Jury :Président
Alain Ibanez
Directeur de recherche, CNRS (– Institut Néel) Rapporteur Yong Chen
Directeur de recherche, Ecole Normale Supérieure (– UMR 8640) Rapporteur Stéphane Veesler
Directeur de recherche, CNRS (CINaM) Examinateur Sladjana Novakovic
Associate Professor, Vinča Institute of Nuclear Sciences Examinateur David Carrière
Directeur de recherche, CEA (– NIMBE) Examinateur Robert B. Pansu
Directeur de recherche, ENS Paris-Saclay (– PPSM) Directeur de thèse Anne Spasojević - de Biré
Professeure, CentraleSupélec (– SPMS) Co-Directeur de thèse
LASER-INDUCED NUCLEATION IN A COAXIAL MICROFLUIDIC MIXER
DISSERTATION
Submitted to the École Doctorale Interfaces of the Université Paris-Saclay in Partial Fulfilment of the Requirements for the Degree of
DOCTOR OF PHILOSOPHY in Chemistry
at
École Normale Supérieure Paris-Saclay by
Zhengyu Zhang
Supervised by Dr. Robert B. Pansu Prof. Anne Spasojević - de Biré
Acknowledgement
More than 8200 kilometres had I flied from Beijing to Paris on September 15, 2015. I can still see that day vividly. My mother saw me off at the Beijing International Airport. It was a long, noisy, and freezing flight. I drank much wine and covered my numb body with my father’s coat. Six o’clock in the morning, Director Robert Pansu was waiting at the Aeroport de Charles de Gaulle. That was the first time I took a plane, the first time I stepped on the land of another country, and the first time Director Pansu and I met in person, although we had had video meetings discussing my master study and my forthcoming PhD. He gave me a quick tour of Paris: l’École Normale Supérieure, la Société Chimique de France…, after which we arrived at l’ENS-Cachan. He introduced me to the lab of PPSM and then drove me to the bank, my dorm, and the supermarket. He took care of a new student like a father would. That gave me the first impression of France: warm, kind, and caring. Yet, on the very next day I was hopelessly lost on the RER B (which reflects another aspect of France) for a meeting with Prof. Anne Spasojević - de Biré.
It was Prof. Spasojević - de Biré who recruited me from Beijing, at which time she was the Dean of the École Centrale de Pékin, and I was in the last year of my master studies on rapid solidification of laser melting deposited titanium in the same university. Looking for a PhD position, I was fascinated by her research on laser-induced nucleation and the polymorphism control by laser polarisation. She accepted my application and arranged several meetings on our campus. I would not pretend that I was not shocked when I first saw her in a wheelchair but then quickly amused, because she ran faster than I through flocks of students, once even raced joyfully with a food delivery guy. Yet, it was not for her driving skills that she was famous among Centralians in Beijing, but for her strictness in teaching. Indeed, she has always been kind to me, letting me pay attention to the cultural gap between France and China, drag me back to the original research plan, explaining the knowledge that I should have learnt before, and sometimes testing me.
fortunately blessed by my research supervisors: Robert and Anne. Professionally, they are always ready to help with the experiment, to answer questions, including stupid ones, and to have discussions. Personally, they have been taking good care of me, helping me fit in the lab and the French society. They are not only my research advisors, but more like my family in France.
I am amazed on a daily basis by Robert’s scope of knowledge and depth of thinking both in and out our field. From him, I have realised that being a scholar is not only about doing experiment and solving equations, but also a way of behaviour, of manner, of language, and of being professional. This can only be learnt through observations: we have been doing experiment together, analysing data together, solving equations together, having lunch together, and attending conferences together. These have been valuable opportunities for me to observe like what a real scientist should be. I treasure this experience as the most important training from my PhD.
I am also amazed on the same daily basis by Anne’s skills, diligence, and strictness. She emphasises on the way of thinking. She has been updating a database of NPLIN related papers filled with the tested compounds, laser types, experimental parameters, results, and proposed mechanisms. She teaches me to rapidly dig pertinent information from literature and to compare with our results. Not only does she work day and night, but also with strictness and efficiency. She urges me to pay attention to details and to timing, for experiments, for writing, and for presentations. She pointed out the smallest flaws in my manuscript, word by word, table to table, figure to figure. I really appreciate that. She is the strongest person I ever know and will always be my inspiration.
in this thesis could have been accomplished if there had not been him.
Many different techniques were involved in our research. I must also extend a huge thank to our collaborators, colleagues, fellow and former students who contributed to this work, notably: Valérie Génot developed the microfluidic device and the first Comsol model; Director Stéphane Veesler is the parrain de thèse, who travelled from Marseille to Paris to check the progress of the thesis at the midterm and gave me advices; Bi Ran measured the solubility of DBDCS, the mixing properties of the solvents, and anti-solvent focusing of Pastis; Prof. Thomas Rodet extracted the fastest FLIM video from our data; Dr. Wenjing Li taught me how to use the NPLIN setup in SPMS; Prof. Soo Young Park’s team synthesised DBDCS and measured its melting point and melting enthalpy; Director Isabelle Leray and Dr. Naresh Kumar synthesised Calix-cousulf; Dr. Javier Perez, Dr. Mehdi Zeghal, Dr. Guillaume Tresset, and Prof. Brigitte Pansu organised a SAXS experiment at the Synchrotron SOLEIL; Evgeny Turbin, Dr. Yury Prokazov, and Dr. Werner Zuschratter have developed and have been maintaining the FLIM detector; Philippe Scouflaire has built and has been maintaining the NPLIN setup in SPMS; Dr. Vu-Long Tran and Dr. Yuanyuan Liao are the first users of the microfluidic device; Dr. Bertrand Clair and Dr. Aziza IKNI are the first users of the NPLIN setup in SPMS; Nada Bošnjaković-Pavlović is currently doing experiments with the NPLIN setup in SPMS; Arnaud Brosseau is the engineer maintaining the spectroscopy room of PPSM; Jean-Pierre Lefèvre is the engineer for the microfluidic room of IDA; Dr. Rasta Ghasemi is the engineer maintaining the SEM of IDA. Thank you all for your help with our research.
It goes without saying that our research would have gone nowhere without the financial support. I am thankful to the Laboratoire Photophysique et Photochimie Supramoléculaires et
Macromoléculaires (PPSM), to the Laboratoire Structures Propriétés, Modélisation des Solides (SPMS), to the Institut d'ALEMBERT, to the ENS Paris-Saclay, to CentraleSupelec, to
I would like to also thank my alma mater, Gansu University of Technology, for giving me strict engineering training. This year is her centennial anniversary. I wish her a happy birthday. I am equally thankful to Beijing University of Aeronautics and Astronautics (BUAA), to Prof. Huaming Wang and Dr. Haibo Tang, and to the National Engineering Laboratory of
Additive Manufacturing for Large Metallic Components. BUAA opened my door from
engineering to academics, from China to France. I have been benefiting day-to-day during my PhD from the training in BUAA: thermodynamics, physical metallurgy, physical chemistry,
mass, heat, and momentum transfer in materials processing, XRD, SEM, DSC, DTA, and so on.
There are not enough words in my English vocabulary to express how much I am grateful to my parents. Not only did they support me through the ups and downs, but it was their education, which cultivated my interest and belief in science. They came to France to support me when I was overwhelmed by the manuscript while my wife was about to give birth. They have done more than enough.
Some special thanks are given to my DD (dear daughter), Xingxian, for her kicking, laughing, crying, vomiting, hiccupping, and pooping, alongside my writing the manuscript. Considering your nine months in the uterus, you accompanied nearly half of my PhD. Thank you for being a lovable rascal. You have my unconditional love, but you need to work hard to gain my respect. I cannot wait to see you become a strong, brave, independent woman.
To my wife
Weixi Wang Zhang
who gives me the best accompany and solace
Abstract
Crystallisation is one of the elementary operations of chemical engineering. Materials are extracted by crystallisation and purified by recrystallisation. But crystal nucleation remains a mystery, and the classical nucleation theory has been undermined by numerous experimental evidences. We have built a microfluidic precipitation device by mixing solvents to produce and continuously observe the birth of a large number of crystals. The molecule chosen for the study is DBDCS, which is fluorescent in solid state (aggregates, crystals, …), but not in solution. Its nuclei will thus be the first luminous object in the mixture.
We have calculated the thermodynamics of the ternary mixture of water (1)-1,4-dioxane (2)-DBDCS (3) from what is known for the binary mixture of 1-2 and the solubility curve of 3 in 1-2, using a two-body-three-body interaction model. From that we have estimated the diffusion coefficients for Comsol simulation. The thermodynamics of the ternary mixtures hypothesised a liquid phase of 3.
A parametric sweep of the microfluidic parameters was carried out. Three types of spontaneous phase transitions from liquid have been recorded: i) nano-particles; ii) droplets; iii) crystals. By plotting the observations as a function of the average composition of the mixture, a working phase diagram of 1-2-3 in the microfluidic system has been established. Droplets prevail on the phase diagram. The volume fraction of the droplets obeys the lever rule of phase separation to a supersaturated solution and a nearly pure liquid phase of DBDCS (3). The liquid-liquid phase separation requires a strong supersaturation following the diffusion of water (1). The study of the solubility of 3 in 1-2 shows that the chemical potential of DBDCS (3) in water (1) is 17.4 RT higher than that in 1,4-dioxane (2). The diffusion of 1 in 2 induces the formation of an energy barrier that repels and concentrates 3 towards the flow centre. Numerical simulation shows that the supersaturation ratio at the flow centre where the liquid-liquid phase separation occurs is beyond 50 and reaches up to 106 order of magintue. The product of this
of the same size.
As the fraction of 2 increases in the anti-solvent, the potential barrier starts to be outweighed by the configurational entropy of mixing. This is shown by the distribution of the fluorescence of the molecules (𝑦𝑖𝑒𝑙𝑑 < 10−4). About five seconds out from the injection
nozzle, the formation and growth of crystals is observed. The numerical simulation indicates that for crystallisation the supersaturation ratio does not exceed 3.5. Rapid imaging and fluorescence lifetime imaging allow the crystals to be observed one by one. Three different polymorphs are identifiable by fluorescence lifetime: the green and the blue phases already reported, and a short-lived phase. The growth rates are widely dispersed, making it difficult to locate and to observe spontaneous nucleation.
Résumé
La cristallisation est une des opérations élémentaires du génie chimique. Les matières produites sont extraites par cristallisation et purifiées par recristallisation. Mais la nucléation du cristal reste un mystère et la théorie classique de la nucléation est battue en brèche par de nombreuses données expérimentales. Nous avons construit un dispositif microfluidique de précipitation par mélange de solvants pour produire de manière continue et observer la formation d’un grand nombre de cristaux. La molécule étudiée est le DBDCS dont les cristaux sont fluorescents mais pas la molécule. Le germe sera ainsi le premier objet lumineux du mélange.
Nous avons calculé la thermodynamique du mélange ternaire DBDCS-1,4-dioxane-eau à partir de ce qui est connu pour le mélange 1,4-dioxane-eau et de la courbe de solubilité du DBDCS dans 1,4-dioxane-eau, dans le cadre du modèle H3M. Ceci nous a permis de fournir a
Comsol les valeurs des coefficients de diffusion du mélange ternaire. La thermodynamique des
mélange ternaires postule une phase liquide du DBDCS.
Nous observons cette phase dans une expérience de précipitation après 1ms de mélange. La mesure du volume de cette phase liquide confirme qu’elle est pratiquement pure. L’apparition de cette phase liquide nécessite une forte sursaturation. Celle-ci fait suite à la diffusion de l’eau qui repousse et concentre le DBDCS au centre du dispositif. L’étude du temps mis à atteindre la concentration critique en fonction de la concentration initiale en DBDCS dans le flux central permet d’obtenir une valeur de 50 à 70 fois la saturation pour la concentration critique d’apparition de la phase liquide DBDCS. Le produit de cette décomposition liquide-liquide est un nuage de gouttelettes sub-micrométriques. Mais le gradient de potentiel chimique peut, dans certaines conditions, regrouper ces nano-gouttes en un chapelet de gouttes micrométriques de même taille.
de la fluorescence résiduelle des molécules (rendement<10-4). Sur des temps de l’ordre de 5s,
on observe la formation et la croissance de cristaux dans un mélange localement homogène. La simulation numérique indique que dans ces conditions la sursaturation relative ne dépasse pas 3,5. L’imagerie rapide et la fluorescence permettent d’observer les cristaux un par un. Trois polymorphes différents sont identifiables par leur durée de vie : les phases vertes et bleues déjà observées et une phase de courte durée de vie. Ces cristaux présentent une vitesse de croissance moyenne proportionnelle à la concentration locale.
En focalisant un laser sur les nuages de nano-gouttes, on observe un effet de pince optique capable de rassembler ces gouttes. En focalisant ce laser dans la zone de super-saturation maximale dans des conditions de nucléation spontanée, on observe une multiplication du nombre de cristaux formés d’un facteur cinq. Nous sommes en présence d’une nucléation induite par laser. Ces cristaux présentent la même vitesse de croissance, la même distribution en nombre des polymorphes, que les cristaux obtenus spontanément. Cette nucléation induite par laser est donc très douce et induit un changement minimal du mécanisme de la nucléation. Un effet de pince optique qui concentre localement les précurseurs du germe et augment transitoirement la sursaturation pourrait avoir cet effet.
Table of contents
1.1. Crystallisation from solution ... 7
1.1.1. Generalities ... 7
1.1.2. Nucleation theories ... 8
1.2. Non-photochemical laser-induced nucleation (NPLIN) ... 16
1.2.1. Necessity for control nucleation ... 16
1.2.2. NPLIN: definition and literature ... 17
1.2.3. NPLIN: characterisation techniques ... 21
1.3. Microfluidics ... 22
1.3.1. Two phases microfluidics ... 22
1.3.2. Crystallisation in microfluidics ... 25 1.4. Fluorescence ... 26 1.4.1. Electronic states ... 26 1.4.2. Jablonski diagram ... 27 1.4.3. Fluorescence yield ... 28 1.4.4. Fluorescence lifetime ... 29
1.4.5. Solid state fluorescence ... 30
1.4.6. Video fluorescence lifetime imaging microscopy (FLIM) ... 34
1.5. (2Z,2'Z)-2,2'-(1,4-phenylene)bis(3-(4-butoxyphenyl) acrylonitrile) (DBDCS) ... 35
1.5.1. Synthesis... 35
1.5.2. Characterisation ... 36
1.5.3. Photoluminescent properties ... 37
2.1. A diffusive coaxial microflow antisolvent precipitation system ... 46
2.1.1. Reactive part of the coaxial microflow mixer ... 46
2.1.2. Flow control in the microfluidic system ... 50
2.1.3. Structure of the coaxial microflow ... 56
2.1.4. Assembling the microfluidic system ... 61
2.2. Laser and microscopy setup for microfluidic NPLIN and FLIM ... 63
2.3. Microfluidic parametric sweep and NPLIN ... 67
Chapter conclusion ... 71
3.1. Molar excess mixing volume, dynamic viscosity, and refractive indices by Redlich-Kister equation ... 76
3.2. Thermodynamics of antisolvent-solvent-solute ternary mixing ... 80
3.2.1. Ideal mixing model ... 80
3.2.3. H3M model for real solvent mixing ... 90
3.2.4. Jouyban-Acree equation for solubility prediction of slightly soluble solute in aqueous-organic mixture with H3M model ... 91
3.3. Appling the H3M model to water (1)-1,4-dioxane (2)-DBDCS (3) irregular ternary system ... 93
3.3.1. Solubility of DBDCS in water (1)-1,4-dioxane (2) mixture ... 93
3.3.2. Thermodynamic parameters of water (1)-1,4-dioxane (2)-DBDCS (3) ternary system 95 3.4. Brief introduction to thermodynamics of diffusion ... 100
3.4.1. Intrinsic diffusion coefficient... 100
3.4.2. Mutual diffusion coefficients ... 105
3.5. Diffusion of water (1)-1,4-dioxane (2)-DBDCS (3) mixture ... 107
3.5.1. Estimation of the diffusion coefficients of water (1)-1,4-dioxane (2) binary system with Moggridge equation ... 107
3.5.2. Estimation of the diffusion coefficient of DBDCS in binary system of water (1)-1,4-dioxane (2) ... 109
3.6. Thermodynamic stability of water (1)-1,4-dioxane (2)-DBDCS (3) ternary mixture ... 113
3.6.1. Liquid-liquid phase separation (LLPS) ... 113
3.6.2. Crystallisation from antisolvent-solvent mixture ... 124
Chapter conclusion ... 125
4.1. Comsol simulation model of the coaxial microflow mixer ... 129
4.1.1. Model ... 129
4.1.2. Parameters ... 132
4.1.3. Studies ... 133
4.2. Simulation of the inter-diffusion of water (1)-1,4-dioxane (2) binary system without DBDCS ... 134
4.2.1. Central jet radius... 134
4.2.2. Flow entrance length ... 136
4.3. Simulation of the diffusion of DBDCS in a field of solvent composition ... 140
Chapter conclusion ... 143
5.1. Phenomena observed in the coaxial microfluidic mixer ... 147
5.2. Evidences for antisolvent focusing of DBDCS ... 148
5.3. Phase diagram of water (1)-1,4-dioxane (2)-DBDCS (3) the coaxial microfluidic mixer ... 151
5.4. The soluble region... 153
5.5. Nano-objects ... 154
5.5.1. In situ OM observation ... 154
5.5.2. Nature of the nano-particles ... 157
5.5.3. Post-mortem observation ... 158
5.6. Liquid-liquid phase separation ... 159
5.6.1. From nanoparticles to droplets ... 159
5.6.2. Formation mechanism of the droplets ... 161
5.6.3. Abnormally large, backward flowing droplets, inner structure and crystallisation of the droplets caught in flow by Marangoni effect. ... 163
5.6.4. Post-mortem drying of the droplets ... 168
5.6.5. Solidification of the droplets in the flow... 169
5.7. Kinetic characteristics of the coaxial microflow mixer ... 170
5.7.1. A simple relation to calculate the droplet formation distance and the average focusing velocity. ... 172
5.7.3. Dependence of LLPS and nano-precipitation starting position on microfluidic
parameters ... 185
5.7.4. Quality of the prediction of the chemical potential focusing velocity, distance, the binodal LLPS threshold and the diffusion coefficient of DBDCS in water (1)-1,4-dioxane (2) coaxial microflow ... 189
5.8. Droplet size dependence on microfluidic parameters ... 192
5.8.1. The total volume fraction of the droplets in the flow ... 192
5.8.2. The size of the DBDCS droplets ... 196
Chapter conclusion ... 203
6.1. Spontaneous crystallisation from a homogeneous microflow ... 207
6.2. Crystal habits of DBDCS ... 208
6.2.1. Spontaneous crystals in the flow... 208
6.2.2. Post-mortem observation ... 211
6.2.3. Heterogeneous crystallisation on the wall of the microfluidic channel ... 212
6.3. FLIM map of spontaneous crystallisation of DBDCS in microflow... 214
6.4. Counting and identifying flowing fluorescent particles with the fastest FLIM video ... 224
6.5. Measuring DBDCS crystal size by FLIM ... 227
6.6. The birth rate and growth rate of spontaneous DBDCS crystals in the microflow of water (1)-1,4-dioxane (2) mixture ... 230
6.6.1. Comsol simulation of the environment ... 230
6.6.2. Definition of the variables ... 231
6.6.3. By FLIM ... 233
6.6.4. By OM ... 237
6.7. Summary of all the spontaneous phase transition types observed in the coaxial microfluidic system... 242
Chapter conclusion ... 244
7.1. Laser-induced crystals ... 248
7.1.1. Early stage of laser-induced nucleation ... 248
7.1.2. Nucleation rate, growth rate and polymorph distribution of laser-induced crystals in microfluidics ... 252
7.1.3. Impact of laser parameters on laser-induced crystallisation in microfluidics ... 261
7.1.4. Post-mortem characterisation of NPLIN crystals ... 272
7.2. Laser’s effect on LLPS and droplets ... 273
7.2.1. Laser dragging the central-peripheral flow interface ... 273
7.2.2. Laser accelerating the phase separation and droplets formation ... 274
7.2.3. Laser releasing the abnormally large droplets from the “droplet trap” ... 276
7.2.4. Laser changing the size of the stable droplets ... 278
7.3. Effect of the focused IR laser of nano-objects ... 279
7.3.1. Dark line ... 279
7.3.2. Laser-induced two-step crystallisation: droplets→crystals ... 280
7.3.3. Laser-induced bubbles on nano-precipitates’ surface ... 282
7.3.4. Impact of laser induction position... 284
7.4. Other observation with the femtosecond IR laser ... 286
7.4.1. Laser tweezers ... 286
7.4.2. Bubbles, explosion, laser ablation. ... 287
7.5. NPLIN working phase diagram ... 288
Discussion ... 294
On the experimental device ... 294
On the thermodynamic calculations and the Comsol simulations ... 295
On the quantitative description of the LLPS ... 295
On the properties of the ternary system water (1)-1,4-dioxane (2)-DBDCS (3) obtained spontaneously in the coaxial microfluidic device. ... 299
On the properties of the ternary system water (1)-1,4-dioxane (2)-DBDCS (3) laser-induced in the coaxial microfluidic device. ... 304
On the polymorphism of DBDCS ... 306
On the different crystallisation techniques... 309
On the different methods for producing droplets ... 311
On the NPLIN mechanism ... 313
On the crystallisation mechanism ... 313
On the potentiality of our method ... 314
Perspectives ... 316
On a better understanding of DBDCS ... 316
On the improvements of our experimental device ... 318
On the improvements of methodologic developments ... 320
Towards the understanding the mechanism of nucleation ... 321
Table of nomenclatures
Notation Definition Unit
Latin letters
a, b, c lattice length parameter m
A
area m2m
A
molar surface area m2∙mol-1x
B
accumulative crystal birth rate from nozzle to x μm s-1 21
x x
B sectional crystal birth rate during x1~x2μm from
nozzle s
-1∙m-1 c , p
subscripts “c” and “p” denote central and peripheral flows, respectively
d
distance mL
d
distance from nozzle to the induction laser focal point mN
d
distance between two successive nucleation events inmicroflow m
P
d
phase transition starting distance from nozzle mD
diameter mF
i
D intrinsic diffusion coefficient of species i m2∙s-1 F
ij
D mutual diffusion coefficient of species i and j m2∙s-1
D diffusion coefficient in infinite dilute solution m2∙s-1 *
D self-diffusion coefficient m2∙s-1
f hydrodynamic factor of maximum central flow radius 1
rep
f laser pulse repetition rate Hz
F
force NA
g
crystal area growth rate m2∙s-1L
g
crystal linear growth rate m∙s-1m
G
molar Gibbs energy J∙mol-1L v
G volume Gibbs energy of liquid phase J∙m-3
s v
G volume Gibbs energy of solid phase J∙m-3
L
sGv
volume Gibbs energy change from liquid to solid J∙m-3 N
G
Gibbs energy change of a nucleus J* N
G
nucleation energy barrier
melt
H
v
volume melting enthalpy J∙m-3r
H
m
molar enthalpy of a reaction J∙mol-1I
optical intensity W∙m-2I
identity tensor, matrixj flux in moving coordinate system kg∙m-2∙s-1
J
flux in fixed coordinate system kg∙m-2∙s-1k
rate constantFRET
F
k
fluorescence decay rate constantIC
k
rate constants of internal conversionISC
k
rate constants of intersystem crossingISOM
k
rate constants of isomerisationN
K
nucleation rate constantQ
k quenching rate constant
c
l
concentration entrance length mh
l
hydrodynamic entrance length mc
L
length of a crystal mi
M
molar mass of species i kg∙mol-1n
M
mean molar mass kg∙mol-1n
amount molD
n
refractive index 1N
number of particles 1*
N number of nuclei per unit volume m-3
ab
N
number of photons absorbed 1em
N
number of photons emitted 1H
N
heterogeneous nucleation rate m-3∙s-1L
N
Laser-induced nucleation rate m-3∙s-1S
N
spontaneous nucleation rate m-3∙s-1p
probability 1avg
P laser average power W
Pe
Péclet number 1peak
P laser peak power W
Q flow rate m3∙s-1
A
Q
activation energy J∙mol-1c
Q
central flow rate m3∙s-1mix
Q
loss of flow rate after mixing of solvents m3∙s-1 pQ peripheral flow rate m3∙s-1
r
radius mr critical radius m
3
r radius of liquid DBDCS molecules m
c,max
r maximum radius of a jet m
drop
r radius of droplet m
o
r
radius of a cylindrical tube before it breaks in todroplets m
channel
R
radius of a microfluidic channel mRe
Reynolds number 1FRET
m
R
molar refractivity m3∙mol-1S
singlet stater
S
m
molar entropy change of a reaction J∙mol-1∙K-1t time s
I
t
induction period sN
t
nucleation event time interval sT
triplet stateT
temperature K T Transpose of a matrix meltT
melting point KT
supercooling Kv
velocity field m∙s-1v
advective velocity of a laminar flow m∙s-1effective
v
effective velocity of a laminar flow m∙s-1max
v
maximum flow velocity of a laminar flow m∙s-1F
v diffusive velocity m∙s-1
F r
v
average antisolvent focusing velocity of a solute m∙s-1V
volume m3m
V
molar volume m3∙mol-1mix
V
m
excess molar mixing volume m3∙mol-1w
focused laser beam radius mi
x
amount fraction of species i 1s
x
amount fraction solubility 1b
i j
x amount fraction binodal decomposition limit of
species i in j 1
s
i j
x amount fraction solubility of species i in j 1
spin
i j
x amount fraction spinodal decomposition limit of
species i in j 1
, ,
x y z
Cartesian coordinates, ,
x r
horizontal cylindrical coordinates Greek letters
, , lattice angle parameter °
supersaturation ratio 1
surface tension N∙m-1, J∙m-2sL
interfacial free energy between solid and liquid phase N∙m-1, J∙m-2i
activity coefficient of species i
Hamiltonian operator2
Laplace operator
kinetic viscosity m2∙s-1
period of in the Plateau–Rayleigh instability mem
emission wavelength m
chemical potential J∙mol-1
dynamic viscosity Pa·s
frequency Hz
mass concentration kg∙m-3D
mass density kg∙m-3b
mass concentration binodal decomposition limit kg∙m-3 bi j
mass concentration binodal decomposition of speciesi in j kg∙m
-3
s
solubility in mass concentration kg∙m-3s
i j
mass concentration solubility of species i in j kg∙m-3 spin
mass concentration spinodal decomposition limit kg∙m-3 spini j
mass concentration spinodal decomposition limit ofspecies i in j kg∙m -3
supersaturation kg∙m-3
sum F
fluorescence lifetime s p
laser pulse width si
volume fraction of species i 1o
i
volume fraction of species i without considering thesolute 1
F
quantum yieldOther
inner product operator
outer product operator
integral
partial derivativeList of acronyms and abbreviations
ABS acrylonitrile butadiene styreneac alternating current
AIE aggregation-induced emission
ATR-FTIR attenuated total reflectance Fourier-transform infrared spectroscopy
BF bright field
CCD charge-coupled device
CL circular left-handed
CMOS complementary metal–oxide–semiconductor CNT classical nucleation theory
CP crossed polarisers
CR circular right-handed
CW continue wavelength
DBDCS (2Z,2'Z)-2,2'-(1,4-phenylene)bis(3-(4-butoxyphenyl) acrylonitrile)
dc direct current
DLS dynamic light scattering
DSC differential scanning calorimetry
DVP divinyl benzene
EF electric field
ENS Paris-Saclay École Normale Supérieure Paris-Saclay FBRM beam reflectance measurement
FEP fluorinated ethylene propylene
FLIM fluorescence lifetime imaging microscopy FRET Förster resonant energy transfer
fs femtosecond
HEWL hen-egg white lysozyme
IC internal conversion
ID inside diameter
IR infrared
ISC intersystem crossing
ISOM isomerisation
LLPS liquid-liquid phase separation
NA numerical aperture
NIR near-infrared
NPLIN non-photochemical laser-induced nucleation
OD optic density
OD outside diameter
OM optical microscopy
PCA principal component analysis
PDMS polydimethylsiloxane
PEEK polyether ether ketone
PNC pre-nucleation cluster
POTS 1H,1H,2H,2H-perfluorooctyltriethoxysilane
PPSM Laboratoire de Photophysique et Photochimie Supramoléculaires et Macromoléculaires
PVM particle vision and measurement
ROI region of interest
SAXS small angle X-ray scattering SEM scanning electron microscopy
SPMS Laboratoire Structures Propriétés et Modélisation des Solides ssNMR solid-state nuclear magnetic resonance
SVA solvent vapor annealing
TEM transmission electron microscopy TICT twisted intramolecular charge transfer
TPE tetraphenylethylene
TSCSPC time- and space- correlated single photon counting TST two-step nucleation theory
UV ultraviolet
vr vibrational relaxation
WF wide-field
WD working distance
Table of physical constants
Quantity Symbol Value Unit
Elementary charge
e
1.602 176 487(40) × 10−19 CFaraday constant
N
A
e
F
96 485.3399(24) C∙mol-1Boltzmann constant
R N
/
Ak
B 1.380 6504(24) × 10−23 J∙K-1Avogadro constant
N
A 6.022 141 79(30) × 1023 mol-1List of figures
Figure 1.1. Chronology of scientists and their contributions towards understanding
nucleation. (Adapted from [Kathmann, 2005])... 8
Figure 1.2. Sketch of the Gibbs energy gain
G
Nas a function of the crystalline
nucleus size r. (Adapted from [Sosso, 2016]) ... 12
Figure 1.3. Schematic comparison of the Gibbs energy gain
G
Nand the structural
change in terms of the cluster size r (Adapted from [Sosso, 2016]) ... 15
Figure 1.4. Schematic definition of NPLIN used in this manuscript. ... 18
Figure 1.5. Growth of the papers on NPLIN according to our extended definition. . . 18
Figure 1.6. Distribution of NPLIN papers according to the compounds studied. ... 19
Figure 1.7. Some key-figures of NPLIN setups.. ... 20
Figure 1.8. Schematic representation of NPLIN sample-holders. ... 21
Figure 1.9. The movement of the flow around a drop of DVB in a gradient of water
(channel wall) and ethanol (channel centre). (Adapted from [Hajian, 2015]) ... 25
Figure 1.10. Schematic representation of the electron in the ground or excited state. 26
Figure 1.11. Schematic energy levels in atoms, molecules, and semiconductors.
(Adapted from [Douglas, 2013])... 27
Figure 1.12. Simple Jablonski diagram illustrating the primary deactivation processes
occurring upon excitation. Electronic levels are represented by heavy lines. (Adapted
from [Douglas, 2013]) ... 28
Figure 1.13. Effect of defects in a fluorescent crystal. ... 32
Figure 1.14. Molecular structure of DBDCS. ... 36
Figure 1.15. Schematic illustration for the preparation of DBDCS using a reactive
inkjet printing method. (Adapted from [Jeon, 2015]) ... 36
Figure 1.16. IR spectral change in DBDCS film due to the UV irradiation or heating.
The asterisk indicates the band of CO
2. (Adapted from [Fujimori, 2016]) ... 37
Figure 1.17. Photo of DBDCS crystals. (Adapted from [Yoon, 2010]) ... 38
Figure 1.18. Fluorescence microscope images of DBDCS spots after 24 h at different
temperatures on glass and PDMS films (𝜆ex 330~385 nm). (Adapted from [Jeon,
2015]) ... 38
Figure 1.19. The absorption and fluorescence spectra of DBDCS in CHCl
3. (Adapted
Figure 2.4. Parameters of the coaxial microfluidic mixer. ... 53
Figure 2.5. Clogging of the borosilicate syringe after a long time of experiment. A:
clogging by caesium acetate in THF-water microflow; B: clogging by DBDCS
precipitation in water (1)-1,4-dioxane (2). ... 54
Figure 2.6. Loss of flow rate after mixing coflow of water (1)-1,4-dioxane (2) and of
water (1)-THF (2) calculated using equation 2.9 in terms of volume fractions. ... 56
Figure 2.7. Central flow jet shape after injection nozzle. ... 58
Figure 2.8. Central flow maximum radius as function of central/peripheral flow ratio.
Data is well described by equation (2.14). ... 59
Figure 2.9. Design from the supporter for the microfluidic capillaries. ... 62
Figure 2.10. Assembled diffusive coaxial microflow antisolvent precipitation system.
... 63
Figure 2.11. Schematic illustration of the laser and microscopy setup for microfluidic
NPLIN and FLIM ... 64
Figure 2.12. Laser and microscope setup for microfluidic NPLIN and FLIM mounted
with the microfluidic system. ... 67
Figure 2.13. Parametric matrix of the experimental inputs and outputs for water
(1)-1,4-dioxane (2)-DBDCS (3) system. * denotes supersaturated mother solution. ... 68
Figure 2.14. Calliper fixed on the microscope stage to measure distance in the
microflow. ... 69
Figure 2.15. Adjustable microscope stage movement blocker (in the red circle). ... 70
Figure 2.16. The microfluidic system mounted on X-ray line SWING of synchrotron
Soleil. ... 71
Figure 3.1. Molar excess mixing volume of water (1)-1,4-dioxane (2) binary mixture
at 298.15 𝐾 [Aminabhavi, 1995]... 77
Figure 3.2. Estimation and experimental values of the mixing properties of water
(1)-1,4-dioxane (2) binary system at 298.15 𝐾. ... 80
Figure 3.3. Stability of ideal solutions.
mixGmof ideal binary (A) and ternary (B)
Figure 3.14. Thermodynamic stability of the binary system of DBDCS and
1,4-dioxane at 298.15 K. ... 118
Figure 3.15. Thermodynamic stability of the binary system of DBDCS and water at
298.15 K. ... 120
Figure 3.16. Stability of water (1)-1,4-dioxane (2)-DBDCS (3) ternary mixture... 122
Figure 3.17. A calculated ternary phase diagram of water (1)-1,4-dioxane (2)-DBDCS
(3).. ... 124
Figure 3.18. Zoom in of the Gibbs energy of DBDCS in water (1)-1,4-dioxane (2)
mixture near the soluble domain. ... 125
Figure 4.1. Axisymmetric geometry of the simulation domain of the reactive part of
the coaxial microflow mixer. ... 130
Figure 4.2. An example of the parametric sweep simulation:
3c= ,
0
Q =
c370 nl min
,
1p 100%
=,
Q =p 1μl min... 134
Figure 4.3. Comparison of the OM images and Comsol simulation of the refractive
index
n of a parametric sweep of a central flow of 1,4-dioxane into a peripheral flow
Dof water. The microfluidic parameters are marked on the small OM images. ... 135
Figure 4.4. Comparison of the Comsol simulation (■), theoretical calculation (line)
and the experimental measurement (▲) of the maximum central jet
rc,maxas a function
of flow ratio... 136
Figure 4.5. Comsol simulation of the development of a laminar flow of a Poiseuille
velocity profile along its radius... 137
Figure 4.6. Parametric sweep simulation of flow velocity profiles along tube centre
(top) and its gradient (bottom) on the flow direction. The hydrodynamic entrance
length
l is 200 µm. ... 138
hFigure 4.7. Comsol simulation of the development of a homogeneous concentration..
... 139
Figure 4.8. Parametric sweep simulation of 1,4-dioxane mass concentration along
flow centre (top) and its gradient (bottom) on the flow direction. This reflects the
concentration entrance length
l of the flow. ... 140
cFigure 4.9. Simulation of DBDCS diffusion in a field of solvent composition... 141
Figure 4.10. Simulation of DBDCS diffusion in a field of solvent composition. ... 143
Figure 5.1. Typical phenomena observed in the coaxial microfluidic mixer with water
(1)-1,4-dioxane (2)-DBDCS (3) system. ... 147
Figure 5.2. A whole image of the demixing. ... 149
Figure 5.3. Evidences and simulation for antisolvent focusing of DBDCS. ... 150
Figure 5.4. Working phase diagram of water (1)-1,4-dioxane (2)-DBDCS (3) phase
diagram in the microfluidic mixer measured by a parametric sweep. ... 152
Figure 5.5. Precipitation of a vague line and its disappearance because the diffusion of
solute driven by the anti-solvent composition gradient, frames taken from a video
moving along the flow. ... 154
Figure 5.6. A column of DBDCS nano-particles formed along the flow centre. ... 156
Figure 5.7. By blocking the microfluidic channel, the flow was temporarily stopped,
and the nano-particles were “frozen” in the suspension. ... 156
Figure 5.8. Precipitation of a dark line later dispersed in to a column of nanoparticles,
frames taken from a video along the flow. ... 157
Figure 5.9. In situ OM transmission image (left) and CP image (right) of the
Figure 5.10. Drying process of a suspension of DBDCS nano-particles collected on a
glass slide. ... 159
Figure 5.11. A~C: post-mortem SEM image of DBDCS nano-particles collected on
copper grid; D~F: bigger objects appeared among nano-particles after 1 month. ... 159
Figure 5.12. Nanoparticles gathered to be droplets. ... 160
Figure 5.13. Droplets along the flow. ... 161
Figure 5.14. Zoom of formation of droplets. A: droplets appeared from the centre of
the microfluidic channel and then grow and merge to a stable size. ... 162
Figure 5.15. Direct breaking of the centre flow by a Plateau–Rayleigh instability. .. 163
Figure 5.16. Frames taken from a video of abnormally large droplet in trapped by
Marangoni effect with t the elapsed time in the video.. ... 164
Figure 5.17. A: abnormally large droplet dragged to the tip by the strong Marangoni
effect and left remanence on the nozzle; B: abnormally large droplet crystallised and
flushed away by the flow. ... 165
Figure 5.18. Crystallisation of trapped abnormally large crystals observed during a
washing. ... 166
Figure 5.19. Inner structure of the trapped abnormally large droplet.. ... 167
Figure 5.20. Post-mortem OM observation of the droplets ... 168
Figure 5.21. Collected dark line of droplets on glass slide. A: suspension in solvents
mixture; B: dried. ... 169
Figure 5.22. Crystallisation of the liquid DBDCS stacked as a pillar along the flow
centre.. ... 169
Figure 5.23. Two-step crystallisation of caesium acetate in the microfluidic mixer. 170
Figure 5.24. By changing only
Qp,
d was observed to be fixed at
P430 µ𝑚 ... 173
Figure 5.25. Schematic illustration of the movement of DBDCS in the antisolvent
focusing of the coaxial microfluidic mixer. ... 174
Figure 5.26. Dependence of average anti-solvent focusing velocity
Fr
v on microfluidic
input parameters.. ... 178
Figure 5.27. Prediction of slopes as a function of flow ratio. ... 180
Figure 5.28. Dependence of the average anti-solvent focusing velocity of DBDCS on
3c
in the coaxial mixer of water (1)-1,4-dioxane (2) flows. ... 181
Figure 5.29. Dependence of the average anti-solvent focusing velocity of DBDCS on
1p
,
c pQ
Q
, and
in the coaxial mixer of water (1)-1,4-dioxane (2) flows. ... 182
3cFigure 5.30. The chemical potential focusing limit (red) of DBDCS by water
(1)-1,4-dioxane (2) in the working phase diagram of water (1)-1,4-(1)-1,4-dioxane (2)-DBDCS (3) in
coaxial microfluidic mixer. ... 184
Figure 5.31. LLPS and nano-precipitation starting position’s dependence on
microfluidic control parameters. ... 186
Figure 5.32. Dependence of
d on
P and
3c . ... 187
1pFigure 5.33. Droplet formation position as a function of
Q ,
c and
3c . ... 188
1 pFigure 5.34. New prediction of antisolvent focusing velocity and droplet formation
distance with equation (5.4) and (5.5) using fitted parameters. ... 191
Figure 5.35. Size dependence of droplets on
Qp. ... 192
water (1)-1,4-dioxane (2)-DBDCS (3). ... 195
Figure 5.39. Total droplet volume fraction is linear with DBDCS total concentration.
Every millilitre of the droplet phase contains 1.2 g DBDCS. ... 196
Figure 5.40. Surface tension of binary mixture of water (1)-1,4-dioxane (2). ... 199
Figure 5.41. Droplets radius as a function of
and
1 pr . ... 201
0Figure 5.42. Droplet radius measurement vs prediction by Plateau-Rayleigh instability
model... 202
Figure 6.1. Spontaneous crystallisation of DBDCS from water-1,4- dioxane mixture
in the coaxial microfluidic mixer.. ... 208
Figure 6.2. Crystal habit of DBDCS spontaneous crystallisation from water
(1)-1,4-dioxane (2) in the coaxial mixer ... 209
Figure 6.3. Crystal habit of DBDCS spontaneous crystallisation from
water-(THF20-1,4-dioxane80) in the coaxial mixer. ... 210
Figure 6.4. Schematic formation mechanism of the “butterfly” twin crystal habit of
DBDCS in the microflow... 211
Figure 6.5. Drying process of the DBDCS butterfly crystals collected at the end of the
microfluidic channel. ... 212
Figure 6.6. Small crystals grow appeared at the “empty” space. ... 212
Figure 6.7. Heterogeneous DBDCS crystals on the microfluidic channel wall... 213
Figure 6.8. FLIM image of three crystals grown on the wall from a flow of
water-(THF20dioxane80)-DBDCS mixture... 214
Figure 6.9. Fluorescence intensity and lifetime treatment of DBDCS spontaneous
crystals in the microflow of water (1)-1,4-dioxane (2). ... 215
Figure 6.10. A collection of fluorescence decays collected at different position along
the spontaneous crystallisation in the flow ... 217
Figure 6.11. The fluorescence lifetime images collected along the spontaneous
crystallisation in the microflow ... 218
Figure 6.12. Comsol simulation of the volume fraction of water, the solubility, the
mass concentration, and supersaturation of DBDCS in the microflow ... 219
Figure 6.13. The decays collected from different areas on the FLIM map along the
spontaneous crystallisation in the flow ... 220
Figure 6.14. The PCA of the fluorescence decays collected on the FLIM map. ... 221
Figure 6.15. Contribution from the principal components to the fluorescence intensity
in the time trace. ... 222
Figure 6.16. Contribution from the “Oligo” DBDCS and the crystals to the
fluorescence intensity in the two regions of interests along the microflow. ... 223
Figure 6.17. The residuals of the data described by the four components: Microscope,
Molecule, “Oligo” and “CPFluctant”. ... 224
Figure 6.18. The fluorescence intensity (red) and lifetime (blue) signal collected from
the flow centre area. ... 225
Figure 6.19. Fluorescence intensity and lifetime after the correction of the detection
time. ... 226
Figure 6.20. Frames of the fastest FLIM video. ... 227
Figure 6.21. The total number of photons counted per DBDCS crystal versus the
transit time through a virtual line in the flow. ... 228
Figure 6.22. Rotation of crystals in the flow of DBDCS crystals in a mixture of
water-THF in the coaxial microflow.. ... 229
Figure 6.23. Comsol simulation of the mass concentration (solid curve) and
supersaturation (dashed curve) of DBDCS along the flow centre for different
Figure 6.24. Number distribution of the nucleation event time interval,
t , measured
Nby FLIM.. ... 233
Figure 6.25. FLIM measurement of the DBDCS crystal area
A distribution and
caccumulative birth rate
Bxalong the microflow. ... 234
Figure 6.26. The correlation between the fluorescence lifetime of individual particles
and their size for six positions along the flow. ... 236
Figure 6.27. OM measurement of nucleation rate and growth rate of spontaneous
crystallisation versus distant from injection nozzle (bottom axis) and residence time
(top distance). ... 239
Figure 6.28. OM measurement of nucleation rate and growth rate of spontaneous
crystallisation versus distant from injection nozzle (bottom axis) and residence time
(top distance).. ... 241
Figure 6.29. Summary of all the spontaneous phase transition behaviours observed in
the coaxial microfluidic system. ... 243
Figure 7.1. Laser-induced DBDCS crystals from a mixture of water (1)-1,4-dioxane
(2) in the coaxial microfluidic mixer. ... 249
Figure 7.2. FLIM image of the microfliudic NPLIN in Figure 7.1. ... 250
Figure 7.3. The fluorescence decays of DBDCS molecules with and without the IR
femtosecond laser... 251
Figure 7.4. Spontaneous crystallisation and growth of DBDCS along the coaxial
microfluidic mixer without IR laser. ... 253
Figure 7.5. Growth process of the laser-induced crystals along the microfluidic
channel. ... 254
Figure 7.6. Growth process of the crystals induced with half the full laser power. . 255
Figure 7.7. Comparison the nucleation rate and the growth rate between laser-induced
(red) and spontaneous crystallisation (olive) under the same microfluidic conditions in
the coaxial mixer measured by OM. . ... 258
Figure 7.8. Comparison of the FLIM measurement of the laser-induced nucleation
(red) and spontaneous nucleation (blue) of DBDCS in the coaxial microflow. ... 259
Figure 7.9. The fluorescence lifetime distribution (the curve covering the circles
plotted vertically at the distance from nozzle) of laser-induced (red) and the
spontaneous (blue) DBDCS crystals measured along the coaxial microflow.. ... 261
Figure 7.10. Impact of laser induction position. Laser was turned on at different
distance
d to the nozzle.. ... 262
LFigure 7.11. The impact of the laser induction position
d on the laser-induced crystal
Lbirth-rate
B10mm. ... 264
Figure 7.12. Impact of IR laser power
Pavgon induced crystals. Observed 10100 µm
from the nozzle. ... 265
Figure 7.13. Impact of laser average power
Pavgon laser-induced crystal the birth rate
10mm
B
. ... 266
Figure 7.14. Size of laser-induced crystals decreased with laser average power
Pavg.
... 267
Figure 7.15. Impact of laser repetition rate
frepon laser-induced crystals.. ... 269
Figure 7.16. Cross comparison of the impact of laser average power
Pavgon
laser-induced crystal birth rate
B10mmat different repetition rate
frep. ... 270
from water (1)-1,4-dioxane (2) mixture. ... 271
Figure 7.18. Impact of laser polarisation on the accumulative crystal birth rate
B10mmof DBDCS in the coaxial microflow of water (1)-1,4-dioxane (2). ... 272
Figure 7.19. Post-mortem OM image of collected laser-induced crystals on glass
slides. ... 273
Figure 7.20. The effect of the focused femtosecond IR laser on the interface between
the central jet of 1,4-dioxane and the peripheral flow of water. ... 274
Figure 7.21. Impact of focused IR laser on droplet formation... 275
Figure 7.22. A~B: two examples of laser releasing abnormally large droplets from the
droplet trap. C: the process how laser released the trapped droplets.. ... 277
Figure 7.23. By increasing the contrast of the image, it shows laser had induced a dark
line before releasing the suspended large droplet.. ... 278
Figure 7.24. Laser’s effect on the size of the droplets. ... 278
Figure 7.25. Laser induced a dark line in the nano-sized precipitation of DBDCS in
the microflow. ... 280
Figure 7.26. OM transmission image and CP image of laser-induced droplet formation
from amorphous nano-objects and the crystallisation of the droplets later in the
microflow. ... 281
Figure 7.27. Laser-induced explosion dependence on laser average power ... 283
Figure 7.28. Laser-induced explosion dependence on flow velocity... 284
Figure 7.29. Impact of laser induction position on interaction with DBDCS
nano-particles.. ... 285
Figure 7.30. Using the femtosecond IR laser as tweezers to move impurities in pure
water. ... 287
Figure 7.31. A~C: laser-induced explosion, ablation, and bubbles on surface of
absorbing solids; D: capillary wall burnt by long time laser explosion. ... 288
Figure 7.32. Summary of spontaneous phase transition types and the effect of the
focused fs IR laser in the coaxial microfluidic system with some characteristic
parameters of interest are marked on the schemes... 289
Figure 7.33. Microfluidic NPLIN working phase diagram... 291
Figure D.1. Lifetime decay (ns) of “object” produced in the microfluidic device
compared to the literature (black circle). ... 307
Figure D.2. Experimental SAXS spectra of DBDCS crystals in microfluidic device.
... 308
Figure D.3. Theoretical powder X-ray diffraction spectra of DBDCS calculated by
reciprOgraph ... 309
Figure D.4. Extraction of Table S2 from [Yoon, 2010]. The Green and the Blue
phases in ground powder sate are indicated with a coloured border. ... 309
Figure D.5. Schematic illustration of a complete full NPLIN experiment in our
List of tables
Table 2.1. Parameters of mixing volume functions for binary mixtures of water
(1)-1,4-dioxane (2) and water-THF [Aminabhavi, 1995] ... 55
Table 2.2. Average power of the IR laser on the sample plane of different
polarisations (P: parallel to flow; S: vertical to flow; CL: circular left-handed; CR:
circular right-handed)... 66
Table 2.3. Laser and microscope configuration and type of experiment ... 66
Table 3.1. Basic physical properties of the materials in this thesis at 298.15 𝐾:
dynamic viscosity , surface tension
, molar surface
A , density
m
D, refractive
index
n , molar refractivity
DR , molar mass M and molar volume
mV .
m*
denotes
calculation of a solute state. ... 76
Table 3.2. Parameters of mixing functions for binary mixtures of H
2O and
1,4-dioxane[Aminabhavi, 1995] ... 77
Table 3.3. Model constants in the Jouyban-Acree model for water (1)-1,4-dioxane (2)
system [Jouyban, 2007] ... 93
Table 3.4 Recalculation of DBDCS amount fraction solubility, measured by Ran Bi in
mass ratio, in binary system of water (1)-1,4-dioxane (2) ... 93
Table 3.5 Fitting parameters for estimation of
mixGmof water (1)-1,4-dioxane
(2)-DBDCS (3) ternary mixture ... 97
Table 3.6. Curve fitting parameters in Figure 3.8 ... 98
Table 3.7. Curve fitting parameters in Figure 3.6 ... 98
Table 3.8 Curve fitting parameters from solubility in pure solvent ... 99
Table 3.9. Measurement of self- [Holz, 2000] and mutual [Leaist, 2000] diffusion
coefficients of water and 1,4-dioxane at 298.15 𝐾, with
F12
Conditions and Figures are given as examples. ... 310
Table D.11. Different conditions and nucleation methods to obtain droplets from our
microfluidic device in the ternary mixture water (1)-1,4-dioxane (2)-DBDCS (3).
Conditions and Figures are given as examples. ... 311
Table P.1. Examples of experiment to be done on DBDCS solvent-antisolvent
List of appendixes
A.i. Thermodynamic versus kinetic aspect of nucleation ... Appen-1 A.ii. Bibliography description of NPLIN experiment ... Appen-2 A.iii. Experimental techniques for crystallisation observation ... Appen-10 A.iii.i. Classical techniques for crystallisation observation ... Appen-10 A.iii.ii. Techniques for pre-nucleation clusters observation... Appen-11 A.iv. Bibliography of DBDCS characterisation ... Appen-16 A.v. Preliminary test materials ... Appen-18 B.i. Technical details of the microfluidics ... Appen-19 B.i.i. The microfluidic system holder ... Appen-19 B.i.ii. Microfluidic capillaries, connectors, and chambers ... Appen-19 B.i.iii. Pumps system, Harvard Apparatus ... Appen-20 B.ii. Structure of the coaxial microflow ... Appen-20 B.ii.i. Central jet radius... Appen-20 B.ii.ii. Flow entrance length ... Appen-21 B.iii. Assembling the microfluidic system ... Appen-22 B.iii.i. Assembling procedures ... Appen-22 B.iv. Problems related with the microfluidic device ... Appen-27 B.iv.i. Cleanness of the capillaries ... Appen-27 B.iv.ii. Temperature control ... Appen-28 B.iv.iii. Deformation and degradation of the device ... Appen-28 B.iv.iv. Precipitation on the injection nozzle of the central flow ... Appen-29 B.iv.v. Working distance of the objective ... Appen-30 B.iv.vi. Leakage and bubble ... Appen-30 B.iv.vii. Influence of gravity ... Appen-30 B.iv.viii. Flow expansion by the big capillary ... Appen-30 B.v. Technical details of the laser sources and illumination type ... Appen-31 B.v.i. Diascopic illumination for bright field (BF) imaging, KhÖler illumination
typ..… ……….Appen-31 B.v.ii. Episcopic illumination for wide-field fluorescence (ep-fl) imaging and IR focusing: ... Appen-31 B.vi. Technical details of the microscope and optics ... Appen-32 B.vi.i. Microscope ... Appen-32 B.vi.ii. Objective and filters arrangement ... Appen-32 B.vii. Technical details of the sensor and detector ... Appen-33 B.vii.i. CCD camera Retiga R1, QImaging... Appen-33 B.vii.ii. QA–Fluorescence Life time Imaging (FLIM) ... Appen-33 B.viii. Laser power, repetition rate, and laser focal spot intensity profile ... Appen-34 C.i. Thermodynamic activity of water (1)-1,4-dioxane (2) system ... Appen-37 C.ii. Limitation of H3M model and Acree-Jouyban equation ... Appen-37
C.iii. Estimation of the melting point, the solid-liquid phase change enthalpy and
entropy of DBDCS ... Appen-42 C.iv. Recent development on the mutual diffusion coefficient of self-associating species ... Appen-46
D.ii. Justification of separation of the concentration- and composition- driven diffusion by using the migration in electric field model in Comsol ... Appen-52
E.i. FLIM measurement of spontaneous precipitation of Calix-Cousulf-Cs+2
Nucleation is a frontier of chemistry. The classical nucleation theory postulates that the transition state which is at the maximum of the energy barrier on the way to crystallisation is a small crystal. This explains the control of crystallisation by kinetics, the production of various polymorphs, and the existence of an amorphous phase and supersaturated solutions. But there are evidences that contradict this model for not describing the actual crystallisation routes [Karthika, 2016]. Crystal growth and design is still the domain of a knowhow and art.
The control of crystal polymorphism is important in the metal industry for mechanical properties, in the pharmaceutical industry for solubility and bioavailability properties, and in the semiconductor industry for electronic properties.
an electromagnetic term the Gibbs energy.
Recently, the Laboratory Photophysique & Photochimie Supramoléculaires et
Macromoléculaires (PPSM) UMR 8531 du CNRS, l’ENS Paris-Saclay has developed a
microfluidic device for the observation of fluorescent crystals and precipitates [Tran, 2016]. The polymorphs of the fluorescence molecule can be distinguished by their fluorescence lifetimes. The uphill diffusion of the solute by a repulsion by the anti-solvent is a known concept that is included in the fundamental equations of thermodynamic of ternary mixtures [Krishna, 2015]. But this solvent driven segregation has not been put forward as a driving force in microfluidic except for the movement of particles [Hajian, 2015].
The production of nanoparticles has been reviewed [Wang, 2015, Ma, 2017, Tao, 2019] and has produced important synthetic success, for example, the reactive precipitation of magnetic particles in co-flow by Abou-Hassan et al [Abou-Hassan, 2009], from whom we have receive the tube microfluidic approach. Other examples are the reactive precipitation of fluorescent perovskite nanoparticle by Lignos et al [Lignos, 2016] and the precipitation of nanometric fluorescent polymeric sensor by A.Reisch [Reisch, 2018]. But few papers have been published on the mechanism of the production of nanoparticles in microfluidics by solvent shifting. The formation of microdroplets through the gathering on nano droplets was postulated [Aubry, 2009]. This is in this community that the focusing of droplets by the Marangoni effect has been first observed [Hajian, 2015].
The manuscript is organised as following:
Chapter 1 summarises the State of art concerning nucleation, NPLIN, fluorescence imaging (FLIM), and DBDCS molecule.
Chapter 2 describes in detail the Experimental coaxial microfluidic mixer for diffusive
antisolvent precipitation, coupled with a focused IR Laser for NPLIN and a wide-field UV Laser for FLIM. This device will allow a parametric sweep of the different parameters.
Chapter 3 presents the Thermodynamics of water (1)-1,4-dioxane (2)-DBDCS (3)
ternary system used in this work. The molar volume, dynamic viscosity, and refractive indices
of the mixture will be expressed using the Redlich-Kister type equation. After an Introduction to the thermodynamics of antisolvent-solvent-solute ternary mixtures, the Jouyban-Acree equation and the H3M model will be applied to the ternary system of 1-2-3. The thermodynamics of diffusion and its application to the diffusion of 1-2-3 mixture will be discussed. Finally, the thermodynamic stability of 1-2-3 ternary mixture will be addressed.
Chapter 4 exposes the Comsol simulation allowed by the thermodynamic equations developed in the previous chapter. Some preliminary comparisons between predictions and observations are presented.
Chapter 5 exhibits the Part 1 of the Phase diagram of water (1)-1,4-dioxane
(2)-DBDCS (3) system in the coaxial microfluidic mixer: the Non-crystalline phase transition.
After the phenomena observed during the phase transitions by solvent displacement and evidences for antisolvent focusing of DBDCS, a phase diagram of 1-2-3 in the coaxial microfluidic mixer will be established. Then, the soluble region, nano-objects, liquid-liquid phase separation, and kinetic characteristics of the coaxial microflow mixer will be carefully described.
Chapter 6 displays the Part 2 of the Phase diagram of water (1)-1,4-dioxane
(2)-DBDCS (3) system in the coaxial microfluidic mixer: the spontaneous crystallisation. It focuses
FLIM characterisation of spontaneous crystallisation of DBDCS in microflow: the counting and identifying of flowing fluorescent particles (the crystal size, the birth rate, and the growth rate of spontaneous DBDCS crystals). Finally, a schematic summary of the spontaneous phase transition types observed in the coaxial microfluidic system will be given.
Chapter 7 concerns the Laser-Induce Nucleation in Microfluidics. The effects of the focused IR laser on the different objects produced in Chapter 5 (flows, nanodroplets, nanoparticles, and droplets) and Chapter 6 (crystal production) are described. A complete schematic summary of the NPLIN working phase diagram will be drawn.
The last chapter contains a general discussion and conclusion and emphasises the